CN110066674A - A kind of tire pyrolysis breeze and gas and oil separating plant - Google Patents
A kind of tire pyrolysis breeze and gas and oil separating plant Download PDFInfo
- Publication number
- CN110066674A CN110066674A CN201910454036.XA CN201910454036A CN110066674A CN 110066674 A CN110066674 A CN 110066674A CN 201910454036 A CN201910454036 A CN 201910454036A CN 110066674 A CN110066674 A CN 110066674A
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- Prior art keywords
- breeze
- oil
- gas
- gate valve
- oil gas
- Prior art date
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- Granted
Links
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 31
- 239000003921 oil Substances 0.000 claims abstract description 100
- 238000005336 cracking Methods 0.000 claims abstract description 40
- 238000006243 chemical reaction Methods 0.000 claims abstract description 29
- 238000007599 discharging Methods 0.000 claims abstract description 15
- 238000007789 sealing Methods 0.000 claims abstract description 14
- 238000009833 condensation Methods 0.000 claims abstract description 11
- 230000005494 condensation Effects 0.000 claims abstract description 11
- 239000000295 fuel oil Substances 0.000 claims abstract description 10
- 238000004227 thermal cracking Methods 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims description 24
- 238000000034 method Methods 0.000 claims description 9
- 230000008569 process Effects 0.000 claims description 6
- 230000007704 transition Effects 0.000 claims description 5
- 239000003638 chemical reducing agent Substances 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 4
- 230000008034 disappearance Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 5
- 239000010920 waste tyre Substances 0.000 abstract description 5
- 239000006229 carbon black Substances 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 239000002893 slag Substances 0.000 abstract description 4
- 239000003738 black carbon Substances 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 69
- 230000008859 change Effects 0.000 description 2
- 238000011900 installation process Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000010129 solution processing Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention belongs to waste tire thermal cracking processing technology field more particularly to a kind of tire pyrolysis breezes and gas and oil separating plant.It solves the heavy oil of oil gas condensation and breeze in current breeze and gas and oil separating plant and mixes and fail to separate and collect, the technical problem of carbon black transportation work low efficiency, the breeze conveyor screw is connect with cracking reaction kettle, the sealing device is arranged between breeze conveyor screw and FlexbleJoint, oil gas transitional storehouse is connected with FlexbleJoint, it is attached between oil gas transitional storehouse and condensing unit by transportation pipe, it is connect with oil gas transitional storehouse and is additionally provided with choke device and device for discharging, avoid heavy oil and the breeze of oil gas condensation admixed together, breeze after cracking can be exported from defeated slag spiral, achieve the purpose that breeze Oil-gas Separation is collected, it ensure that the feature of environmental protection and continuity in production process, improve waste tire cracking black carbon transportation work efficiency, device moving component is few, energy consumption can be reduced.
Description
Technical field
The invention belongs to waste tire thermal cracking processing technology field more particularly to a kind of tire pyrolysis breezes and oil gas point
From device.
Background technique
Ardent solution processing damaged tire technology be using the hot fume that various industrial waste oils generate or with electric heater unit of burning,
By damaged tire heat resolve, gas recovery, oil, solid carbon, steel wire and some chemical products under anoxic or natural instincts atmosphere.Cracking
Equipment is to realize the place of final cracking reaction, it design be successfully entire technique key point.
Although can obtain the pretty good pyrolysis product of quality in pervious many experimental studies, design meets technique and wants
There is very big difficulty in the cracking apparatus asked, the breeze conveying before waste tire thermal cracking be all from one end of charging, and it is present
Structure be to convey breeze to transport out behind reaction kettle；And having a drawback before conveying below is the oil of thermal cracking
Gas and breeze export together, because breeze conveyor screw discharges inside dregs of fat separation bin, and the oil gas that hot tearing solves mistake herein
It stops to be allowed to cool in journey and generates heavy constituent oil, keep oil and breeze admixed together, the feature of environmental protection and continuity in production process
Difference, carbon black transportation work low efficiency.
Summary of the invention
The present invention provides a kind of tire pyrolysis breeze and gas and oil separating plants, solve current breeze and Oil-gas Separation dress
The heavy oil and breeze for setting middle oil gas condensation mix fail to separate and collect, the feature of environmental protection and poor continuity, carbon black transportation work
The technical problem of low efficiency.
In order to achieve the above object, the present invention provides the following technical scheme that
A kind of tire pyrolysis breeze and gas and oil separating plant, including cracking reaction kettle 1, breeze conveyor screw 2, sealing device
3, FlexbleJoint 4, oil gas transitional storehouse 5, transportation pipe 6, condensing unit 7, electric knives gate valve 1, breeze delivery pipe 9, electricity
Acting knife gate valve 2 10, the breeze conveyor screw 2 are connect with cracking reaction kettle 1, and the setting of sealing device 3 is defeated in breeze
Between square auger 2 and FlexbleJoint 4, oil gas transitional storehouse 5, oil gas transitional storehouse 5 and condensation are connected with FlexbleJoint 4
It is attached between device 7 by transportation pipe 6, is connect with oil gas transitional storehouse 5 and be additionally provided with choke device and device for discharging.
Further, the cracking reaction kettle 1 is the high-temperature cracking furnace for carrying out tire pyrolysis.
Further, the breeze conveyor screw 2 is that have speed reducer to provide power, by helical blade by breeze from splitting
The device transferred out in solution reaction kettle.
Further, the FlexbleJoint 4 is the device for compensating the swell increment of cracking reaction kettle 1.
Further, the oil gas transitional storehouse 5 is that the oil gas transition for will generate after thermal cracking tires is transported to cold
Device in solidifying device 7.
Further, the choke device and device for discharging are by electric knives gate valve 1, breeze delivery pipe 9 and electronic
The closed cavity that knife gate valve 2 10 forms.
Further, the control process of the choke device and device for discharging is as follows: 2 10 initial place of electric knives gate valve
In closed state, when breeze delivery pipe 9 detects the material position of material, stops the conveying of breeze conveyor screw 2, close electric knife gate
Valve 1 opens electric knives gate valve 2 10, material enters after cooling and completes to collect, when the material position of material disappears after completely closing
It loses, closes electric knives gate valve 2 10, open breeze conveyor screw 2, open one 8 material of electric knives gate valve and start to continue to convey.
The operational process of above-mentioned tire pyrolysis breeze and gas and oil separating plant, steps are as follows: the breeze conveyor screw 2
Breeze and oil gas are delivered in sealing device 3 from cracking reaction kettle 1, by the diversion pipe built in FlexbleJoint 4, oil gas
Enter condensing unit 7 from the top of oil gas transitional storehouse 5 by transportation pipe 6, heavy oil and light oil are collected by condensation, and it is described
Breeze be delivered to the outside of oil gas transitional storehouse 5, by electric knives gate valve 1, breeze delivery pipe 9 and 2 10 groups of electric knives gate valve
At choke device and device for discharging in, complete separating and collecting for breeze and oil gas.
Compared with prior art, the invention has the following advantages:
1, the conveying that tire pyrolysis breeze and gas and oil separating plant provided by the invention are related to old tire cracking black carbon is collected
It is efficiently separated with oil gas and the reasonable of carbon black, changes the old traditional handicraft of the mode of slagging tap and the mixing of oil gas breeze, overcome biography
The defect of system technology, it is easy to operate, provide a kind of heavy oil for avoiding oil gas condensation and breeze device admixed together, cracking
Breeze afterwards can be exported from defeated slag spiral, achieve the purpose that breeze Oil-gas Separation is collected, and ensure that environmentally friendly in production process
Property and continuity, improve waste tire cracking black carbon transportation work efficiency, device moving component is few, it is possible to reduce energy consumption, section
About cost.
2, the breeze conveyor screw in tire pyrolysis breeze and gas and oil separating plant provided by the invention is by breeze from cracking
It is delivered to choke device in reaction kettle, realizes effective conveying of breeze, has reached significant effect safe and stable, that continuity is strong
Fruit.
3, the oil gas transitional storehouse in tire pyrolysis breeze and gas and oil separating plant provided by the invention is small in size, avoids oil gas
It cools down herein and generates heavy oil, breeze is delivered on the outside of oil gas transitional storehouse, to realize that breeze and Oil-gas Separation are collected, is improved
The quality of product and the efficiency of production.
Detailed description of the invention
Fig. 1 is tire pyrolysis breeze provided in an embodiment of the present invention and gas and oil separating plant structural schematic diagram；
Note: 1- cracking reaction kettle, 2- breeze conveyor screw, 3- sealing device, 4- FlexbleJoint, 5- oil gas transitional storehouse,
6- transportation pipe, 7- condensing unit, 8- electric knives gate valve one, 9- breeze delivery pipe, 10- electric knives gate valve two.
Specific embodiment
In the following, the present invention is specifically described by illustrative embodiment.It should be appreciated, however, that not into one
In the case where step narration, element, structure and features in an embodiment can also be advantageously incorporated into other embodiments
In.
In the description of the present invention, it is to be understood that, the orientation or position of the instructions such as term " on ", "lower", "bottom", "inner"
Relationship is set to be merely for convenience of description of the present invention and simplification of the description based on attached orientation or positional relationship shown in FIG. 1, rather than
The device or element of indication or suggestion meaning must have a particular orientation, be constructed and operated in a specific orientation, therefore cannot
It is interpreted as limitation of the present invention.
Term " first ", " second " be used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance or
Implicitly indicate the quantity of indicated technical characteristic." first " is defined as a result, the feature of " second " can be expressed or imply
Ground includes one or more of the features.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term
" connected ", " connection " shall be understood in a broad sense, for example, it may be fixedly connected, may be a detachable connection or one
Connect to body；It can be directly connected, the connection inside two elements can also be can be indirectly connected through an intermediary.
For the ordinary skill in the art, the concrete meaning of above-mentioned term in the present invention can be understood with concrete condition.
The embodiment of the present invention provides a kind of tire pyrolysis breeze and gas and oil separating plant, including cracking reaction kettle 1, breeze are defeated
Square auger 2, sealing device 3, FlexbleJoint 4, oil gas transitional storehouse 5, transportation pipe 6, condensing unit 7, electric knives gate valve one
8, breeze delivery pipe 9, electric knives gate valve 2 10, the breeze conveyor screw 2 are connect with cracking reaction kettle 1, the sealing
Device 3 is arranged between breeze conveyor screw 2 and FlexbleJoint 4, is connected with oil gas transitional storehouse 5 with FlexbleJoint 4,
It is attached between oil gas transitional storehouse 5 and condensing unit 7 by transportation pipe 6, is connect with oil gas transitional storehouse 5 and be additionally provided with resistance
Device of air and device for discharging.
Tire pyrolysis breeze and gas and oil separating plant provided in an embodiment of the present invention rationally efficiently separate breeze and oil gas,
The old traditional handicraft of the mode of slagging tap and the mixing of oil gas breeze is changed, device provided in an embodiment of the present invention is easy to operate, keeps away
The heavy oil and breeze for exempting from oil gas condensation are mixed, and the breeze after cracking can be exported from defeated slag spiral, reach breeze oil gas
The purpose separated and collected, it is ensured that the feature of environmental protection and continuity in production process, device movement provided in an embodiment of the present invention
Component is few, it is possible to reduce energy consumption, save the cost.
In an alternative embodiment, the cracking reaction kettle 1 is the high-temperature cracking furnace for carrying out tire pyrolysis.This hair
The high-temperature cracking furnace good airproof performance that bright embodiment provides, is the place of tire pyrolysis.
In an alternative embodiment, the breeze conveyor screw 2 is that have speed reducer to provide power, will by helical blade
The device that breeze is transferred out from cracking reaction kettle.
In an alternative embodiment, the FlexbleJoint 4 has retractility, high temperature resistant, can compensate for cracking reaction kettle 1
Swell increment, while can be adjusted by ripple compensation in installation process.
In an alternative embodiment, the oil gas transitional storehouse 5 is the oil gas transition for will generate after thermal cracking tires
Transport the device into condensing unit 7.Oil gas transitional storehouse is that the oil gas generated after thermal cracking tires enters this by gas outlet
In a transitional storehouse, and then the condensing unit after entrance, pass through condensation and collects heavy oil and light oil.
In an alternative embodiment, the choke device and device for discharging are by electric knives gate valve 1, breeze delivery pipe
9 and electric knives gate valve 2 10 form closed cavity.The electric knives gate valve is easy to operate, and good seal performance is reliable and stable,
Long service life.
In an alternative embodiment, electric knives gate valve 2 10 is initially in closed state, and breeze delivery pipe 9 detects material
Material position when, stop breeze conveyor screw 2 conveying, close electric knives gate valve 1, after completely closing, open electric knife gate
Valve 2 10, material enter after cooling and complete to collect, and when the material position of material disappears, closing electric knives gate valve 2 10 opens breeze
Conveyor screw 2 opens one 8 material of electric knives gate valve and starts to continue to convey.
The operational process of tire pyrolysis breeze and gas and oil separating plant provided in an embodiment of the present invention, steps are as follows: described
Breeze conveyor screw 2 breeze and oil gas are delivered in sealing device 3 from cracking reaction kettle 1, by FlexbleJoint 4
The diversion pipe set, oil gas enter condensing unit 7 by transportation pipe 6 from the top of oil gas transitional storehouse 5, collect weight by condensation
Oil and light oil, and the breeze is delivered to 5 outside of oil gas transitional storehouse, by electric knives gate valve 1,9 and of breeze delivery pipe
In the choke device and device for discharging that electric knives gate valve 2 10 forms, separating and collecting for breeze and oil gas is completed.
Tire pyrolysis breeze and gas and oil separating plant provided by the embodiment of the present invention are introduced in detail in order to become apparent from, under
Face will be described in conjunction with specific embodiments.
Embodiment 1
As shown in Figure 1, a kind of tire pyrolysis breeze and gas and oil separating plant, including cracking reaction kettle 1, breeze conveyor screw
2, sealing device 3, FlexbleJoint 4, oil gas transitional storehouse 5, transportation pipe 6, condensing unit 7, electric knives gate valve 1, breeze
Delivery pipe 9, electric knives gate valve 2 10, the breeze conveyor screw 2 are connect with cracking reaction kettle 1, and the sealing device 3 is set
It sets between breeze conveyor screw 2 and FlexbleJoint 4, is connected with oil gas transitional storehouse 5, oil gas mistake with FlexbleJoint 4
It crosses between storehouse 5 and condensing unit 7 and is attached by transportation pipe 6, connect with oil gas transitional storehouse 5 and be additionally provided with choke device
And device for discharging.The cracking reaction kettle 1 is the high-temperature cracking furnace for carrying out tire pyrolysis.The breeze conveyor screw
2 be to have speed reducer to provide power, the device for transferring out breeze from cracking reaction kettle by helical blade.The ripple is mended
Device 4 is repaid with retractility, high temperature resistant, can compensate for the swell increment of cracking reaction kettle 1, while ripple compensation can be passed through in installation process
It is adjusted.The oil gas transitional storehouse 5 is that the oil gas transition for will generate after thermal cracking tires is transported into condensing unit 7
Device.
Choke device described in the present embodiment and device for discharging are by electric knives gate valve 1, breeze delivery pipe 9 and electronic
The closed cavity that knife gate valve 2 10 forms.Electric knives gate valve 2 10 is initially in closed state, and breeze delivery pipe 9 detects material
Material position when, stop breeze conveyor screw 2 conveying, close electric knives gate valve 1, after completely closing, open electric knife gate
Valve 2 10, material enter after cooling and complete to collect, and when the material position of material disappears, closing electric knives gate valve 2 10 opens breeze
Conveyor screw 2 opens one 8 material of electric knives gate valve and starts to continue to convey.
The operational process of tire pyrolysis breeze and gas and oil separating plant provided in this embodiment, steps are as follows: the charcoal
Breeze and oil gas are delivered in sealing device 3 by slag conveyor screw 2 from cracking reaction kettle 1, by built in FlexbleJoint 4
Diversion pipe, oil gas from the top of oil gas transitional storehouse 5 by transportation pipe 6 enter condensing unit 7, by condensation collect heavy oil and
Light oil, and the breeze is delivered to the outside of oil gas transitional storehouse 5, by electric knives gate valve 1, breeze delivery pipe 9 and electronic
In the choke device and device for discharging that knife gate valve 2 10 forms, separating and collecting for breeze and oil gas is completed.
Although specific embodiments of the present invention have been described above, it will be appreciated by those of skill in the art that these
It is merely illustrative of, what protection scope of the present invention should be limited by claim.Those skilled in the art is without departing substantially from this
Under the premise of the principle and essence of invention, various changes or modifications can be made to these embodiments, but these change and repair
Change and each falls within protection scope of the present invention.
Claims (8)
1. a kind of tire pyrolysis breeze and gas and oil separating plant, it is characterised in that: convey spiral shell including cracking reaction kettle (1), breeze
It revolves (2), sealing device (3), FlexbleJoint (4), oil gas transitional storehouse (5), transportation pipe (6), condensing unit (7), electronic
Knife gate valve one (8), breeze delivery pipe (9), electric knives gate valve two (10), the breeze conveyor screw (2) and cracking reaction kettle
(1) it connects, the sealing device (3) is arranged between breeze conveyor screw (2) and FlexbleJoint (4), with ripple compensation
Device (4) is connected with oil gas transitional storehouse (5), passes through transportation pipe (6) between oil gas transitional storehouse (5) and condensing unit (7)
It is attached, is connect with oil gas transitional storehouse (5) and be additionally provided with choke device and device for discharging.
2. tire pyrolysis breeze according to claim 1 and gas and oil separating plant, it is characterised in that: the cracking reaction
Kettle (1) is the high-temperature cracking furnace for carrying out tire pyrolysis.
3. tire pyrolysis breeze according to claim 1 and gas and oil separating plant, it is characterised in that: the breeze conveying
Spiral (2) is that have speed reducer to provide power, the device for transferring out breeze from cracking reaction kettle by helical blade.
4. tire pyrolysis breeze according to claim 1 and gas and oil separating plant, it is characterised in that: the ripple compensation
Device (4) is the device for compensating the swell increment of cracking reaction kettle (1).
5. tire pyrolysis breeze according to claim 1 and gas and oil separating plant, it is characterised in that: the oil gas transition
Storehouse (5) is that the device into condensing unit (7) is transported in the oil gas transition for will generate after thermal cracking tires.
6. tire pyrolysis breeze according to claim 1 and gas and oil separating plant, it is characterised in that: the choke device
The closed cavity being made of with device for discharging electric knives gate valve one (8), breeze delivery pipe (9) and electric knives gate valve two (10).
7. tire pyrolysis breeze according to claim 6 and gas and oil separating plant, it is characterised in that: the choke device
As follows with the control process of device for discharging: electric knives gate valve two (10) is initially in closed state, and breeze delivery pipe (9) detects
When the material position of material, stop the conveying of breeze conveyor screw (2), close electric knives gate valve one (8), after completely closing, opens
Electric knives gate valve two (10), material enter after cooling and complete to collect, and when the material position disappearance of material, close electric knives gate valve two
(10), breeze conveyor screw (2) are opened, opens electric knives gate valve one (8) material and starts to continue to convey.
8. the operation of tire pyrolysis breeze and gas and oil separating plant described in a kind of any one of -7 claims according to claim 1
Process, it is characterised in that: steps are as follows: the breeze conveyor screw (2) is defeated from cracking reaction kettle (1) by breeze and oil gas
It send into sealing device (3), by the diversion pipe built in FlexbleJoint (4), oil gas passes through from the top of oil gas transitional storehouse (5)
Transportation pipe (6) enters condensing unit (7), collects heavy oil and light oil by condensation, and the breeze is delivered to oil gas mistake
It crosses on the outside of storehouse (5), into the choke dress being made of electric knives gate valve one (8), breeze delivery pipe (9) and electric knives gate valve two (10)
It sets in device for discharging, completes separating and collecting for breeze and oil gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910454036.XA CN110066674B (en) | 2019-05-28 | 2019-05-28 | Tire schizolysis carbon residue and oil gas separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910454036.XA CN110066674B (en) | 2019-05-28 | 2019-05-28 | Tire schizolysis carbon residue and oil gas separation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110066674A true CN110066674A (en) | 2019-07-30 |
| CN110066674B CN110066674B (en) | 2024-04-05 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910454036.XA Active CN110066674B (en) | 2019-05-28 | 2019-05-28 | Tire schizolysis carbon residue and oil gas separation device |
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| CN (1) | CN110066674B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111187635A (en) * | 2020-03-05 | 2020-05-22 | 河南伊克斯达再生资源有限公司 | Carbon black and steel wire separation device, separation method and thermal cracking system |
| CN112371701A (en) * | 2020-11-17 | 2021-02-19 | 河北藏隆再生资源利用有限公司 | Waste tyre oil refining equipment |
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